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filingDate 1990-12-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1992-12-30-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e50e18103f0e226d74b9e2ad32caa2e4
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publicationDate 1992-12-30-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber RU-1785523-C
titleOfInvention The method of obtaining 1,1,2-trichloroethane
abstract Use :: for the production of vinyl denesporide, a valuable monomer SUMMARY OF THE INVENTION Product 1,1,1-tri (Chpor) egan Reagent 11 from the production of vinip lorpda, composition: 1,2-di poretan 20-80%, lorztipene 2-12%, the rest up to 100%. | porous Compounds, reagent 2 ENT “Reaction conditions 80 ° C, initiator is ethipene, recycling of unreacted 1,2-dichloroethane to the stage of chlorination, molar ratio of ethylene-) pore-wastes (0,025-0,4) (0,4- 0.81-1, 3 tab. Disadvantage: the known method consists in obtaining a mixture of TCE isomers. In addition, the feedstock for the preparation contains two isomers, and its processing requires the presence of solvent, which limits the application of this method. A known method for producing TCE is as follows: g., ofaznoy chporirovanie vinyl chloride (B), :) in the environment in pr katapizatora elornogo presence of: -b: -epeea at 20-30 &deg; C under mopprnom soognoshenii "is time and B v 0,8- 1 :: 1 with recycle of unreacted BY. to the beginning of the process And although, in contrast to the previous one, the “technical solution, the chlorination of B” is carried out in the environment of the target product, the disadvantage of the known solution is also the difficulty in obtaining the initial raw material -B, the technological process of ei-ia of which consists of a dehydro-prior stage DCE to BX At this stage, CO is formed with 4
priorityDate 1990-12-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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Total number of triples: 38.